caa a22 4500 388021454 CHVBK 20180307124925.0 cr unu---uuuuu 161130e199802 xx s 000 0 eng 10.1557/JMR.1998.0064 doi S0884291400043016 pii (NATIONALLICENCE)cambridge-10.1557/JMR.1998.0064 Thermal transport due to material and gas flow in a furnace for drawing an optical fiber [Elektronische Daten] The transport processes involved in the neck-down region for optical fiber drawing are numerically investigated. In this manufacturing process, a moving glass rod is heated in a furnace containing an inert gas environment and drawn into a thin optical fiber. The conjugate problem is solved considering both radiation and convection, with focus on the latter. Two different flow configurations, involving inert gas flow in the same as well as in the opposite direction as the moving preform/fiber, are considered in this study. A coordinate transformation is used to change the complicated computational domains in the gas and the fiber to cylindrical ones. The transport in the fiber is coupled with that in the gas through the boundary conditions. The radiative thermal transport is calculated using an enclosure model developed in an earlier study. The numerical results on convective flow and transport are validated by comparing with results available in the literaturefor simpler configurations. The effects of several important parameters such as fiber draw speed, inert gas velocity, furnace dimensions, and gas properties on the flow and temperature distributions are investigated. For the aiding flow case, in which the inert gases flow in the same direction as the fiber, heat transfer to the fiber increases as the gas velocity increases. For opposing flow, a recirculating region appears in the gas, close to the moving fiber surface, causing reduction in heat transfer as compared to the aiding case. The thickness of this recirculating zone decreases with increasing inert gas velocity. Radiation is found to be the dominant mode of heat transfer in the overall heating of the preform/fiber, with nitrogen as the inert gas. However, near the edges of the furnace, radiation heat transfer is relatively small and convection becomes very important. Also, the convective transfer rate is relatively large near the flow entrance because of the large temperature difference between the gas and the fiber. However, away from the entrance, the gas heats up and the temperature difference relative to the fiber decreases, resulting in a smaller convective heat transfer rate. The relevance of the results to various aspects of the fiber-drawing process is discussed. Copyright © Materials Research Society 1998 Roy Choudhury S. Department of Mechanical and Aerospace Engineering, Rutgers University, New Brunswick, New Jersey 08903 Jaluria Y. Department of Mechanical and Aerospace Engineering, Rutgers University, New Brunswick, New Jersey 08903 Journal of Materials Research Cambridge University Press 13/2(1998-02), 494-503 0884-2914 13:2<494 1998 13 JMR https://doi.org/10.1557/JMR.1998.0064 text/html Onlinezugriff via DOI 1 research-article jats NATIONALLICENCE 856 40 https://doi.org/10.1557/JMR.1998.0064 text/html Onlinezugriff via DOI NATIONALLICENCE 700 1- Roy Choudhury S. Department of Mechanical and Aerospace Engineering, Rutgers University, New Brunswick, New Jersey 08903 NATIONALLICENCE 700 1- Jaluria Y. Department of Mechanical and Aerospace Engineering, Rutgers University, New Brunswick, New Jersey 08903 NATIONALLICENCE 773 0- Journal of Materials Research Cambridge University Press 13/2(1998-02), 494-503 0884-2914 13:2<494 1998 13 JMR CC0 http://creativecommons.org/publicdomain/zero/1.0 nationallicence BK010053 XK010053 XK010000 NATIONALLICENCE NATIONALLICENCE NL-cambridge